MX2024000914A - Trifunctional processes in catalytic distillation. - Google Patents
Trifunctional processes in catalytic distillation.Info
- Publication number
- MX2024000914A MX2024000914A MX2024000914A MX2024000914A MX2024000914A MX 2024000914 A MX2024000914 A MX 2024000914A MX 2024000914 A MX2024000914 A MX 2024000914A MX 2024000914 A MX2024000914 A MX 2024000914A MX 2024000914 A MX2024000914 A MX 2024000914A
- Authority
- MX
- Mexico
- Prior art keywords
- alcohol
- feedstock
- unreacted
- olefins
- trifunctional
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
- C07C41/01—Preparation of ethers
- C07C41/09—Preparation of ethers by dehydration of compounds containing hydroxy groups
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/009—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in combination with chemical reactions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/143—Fractional distillation or use of a fractionation or rectification column by two or more of a fractionation, separation or rectification step
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0492—Feeding reactive fluids
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/08—Alkenes with four carbon atoms
- C07C11/09—Isobutene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/10—Alkenes with five carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
- C07C41/01—Preparation of ethers
- C07C41/05—Preparation of ethers by addition of compounds to unsaturated compounds
- C07C41/06—Preparation of ethers by addition of compounds to unsaturated compounds by addition of organic compounds only
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
- C07C41/01—Preparation of ethers
- C07C41/34—Separation; Purification; Stabilisation; Use of additives
- C07C41/40—Separation; Purification; Stabilisation; Use of additives by change of physical state, e.g. by crystallisation
- C07C41/42—Separation; Purification; Stabilisation; Use of additives by change of physical state, e.g. by crystallisation by distillation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C43/00—Ethers; Compounds having groups, groups or groups
- C07C43/02—Ethers
- C07C43/03—Ethers having all ether-oxygen atoms bound to acyclic carbon atoms
- C07C43/04—Saturated ethers
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
- C07C5/03—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of non-aromatic carbon-to-carbon double bonds
- C07C5/05—Partial hydrogenation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/23—Rearrangement of carbon-to-carbon unsaturated bonds
- C07C5/25—Migration of carbon-to-carbon double bonds
- C07C5/2506—Catalytic processes
- C07C5/2562—Catalytic processes with hydrides or organic compounds
- C07C5/2568—Catalytic processes with hydrides or organic compounds with ion-exchange resins
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00893—Feeding means for the reactants
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2531/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- C07C2531/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- C07C2531/06—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
- C07C2531/08—Ion-exchange resins
- C07C2531/10—Ion-exchange resins sulfonated
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/582—Recycling of unreacted starting or intermediate materials
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crystallography & Structural Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Un proceso para la producción de alquil éteres incluye alimentar una materia prima de hidrocarburos y una primera materia prima de alcohol a un reactor de lecho fijo que contiene un catalizador de eterificación. La materia prima de hidrocarburos y la primera materia prima de alcohol entran en contacto en el primer reactor de lecho fijo para hacer reaccionar las isoolefinas con el alcohol en presencia del catalizador de la eterificación para producir un primer flujo de producto. El primer flujo de producto se alimenta junto con una materia prima de hidrógeno y una segunda materia prima de alcohol a un sistema de reacción de destilación catalítica que contiene un catalizador trifuncional para isomerizar concurrentemente al menos una parte de las alfa-olefinas e hidrogenar al menos una parte de las diolefinas y eterificar al menos una parte de las isoolefinas y alcohol, produciendo productos residuales que comprenden uno o más éteres y un producto suspendido que comprende n-alcanos, isoalcanos, alfa olefinas sin reaccionar, olefinas internas sin reaccionar y alcohol sin reaccionar.A process for producing alkyl ethers includes feeding a hydrocarbon feedstock and a first alcohol feedstock to a fixed bed reactor containing an etherification catalyst. The hydrocarbon feedstock and the first alcohol feedstock are contacted in the first fixed bed reactor to react isoolefins with the alcohol in the presence of the etherification catalyst to produce a first product stream. The first product stream is fed together with a hydrogen feedstock and a second alcohol feedstock to a catalytic distillation reaction system containing a trifunctional catalyst to concurrently isomerize at least a portion of the alpha-olefins and hydrogenate at least a portion of the diolefins and etherify at least a portion of the isoolefins and alcohol, producing residual products comprising one or more ethers and a slurry comprising n-alkanes, isoalkanes, unreacted alpha olefins, unreacted internal olefins, and unreacted alcohol.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US202163223614P | 2021-07-20 | 2021-07-20 | |
| PCT/US2022/037620 WO2023003898A1 (en) | 2021-07-20 | 2022-07-19 | Trifunctional processes in catalytic distillation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| MX2024000914A true MX2024000914A (en) | 2024-03-15 |
Family
ID=84976954
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MX2024000914A MX2024000914A (en) | 2021-07-20 | 2022-07-19 | Trifunctional processes in catalytic distillation. |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US20230027740A1 (en) |
| EP (1) | EP4373801A4 (en) |
| JP (1) | JP2024527846A (en) |
| KR (1) | KR20240027799A (en) |
| MX (1) | MX2024000914A (en) |
| WO (1) | WO2023003898A1 (en) |
| ZA (1) | ZA202400697B (en) |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2355792A1 (en) * | 1976-06-25 | 1978-01-20 | Inst Francais Du Petrole | PROCESS FOR ISOMERIZING 1-BUTENE TO 2-BUTENE |
| CA2003404C (en) * | 1988-11-22 | 2002-03-12 | John J. Cikut | Minimizing deactivation of ether synthesis catalyst |
| US5196612A (en) * | 1992-02-03 | 1993-03-23 | Uop | Etherification of isoamylenes by catalytic distillation |
| US5523272A (en) * | 1994-08-19 | 1996-06-04 | Intevep, S.A. | Catalyst and process for the production of alkyl tert alkyl ether from hydrocarbon feedstocks with high levels of sulfur |
| US5628880A (en) * | 1996-02-12 | 1997-05-13 | Chemical Research & Licensing Company | Etherification--hydrogenation process |
| US6262314B1 (en) * | 1999-04-06 | 2001-07-17 | Intevep, S.A. | Process for preparation of ethers in a catalytic distillation column |
-
2022
- 2022-07-19 KR KR1020247003561A patent/KR20240027799A/en active Pending
- 2022-07-19 JP JP2024503720A patent/JP2024527846A/en active Pending
- 2022-07-19 MX MX2024000914A patent/MX2024000914A/en unknown
- 2022-07-19 WO PCT/US2022/037620 patent/WO2023003898A1/en not_active Ceased
- 2022-07-19 EP EP22846523.3A patent/EP4373801A4/en active Pending
- 2022-07-20 US US17/813,614 patent/US20230027740A1/en active Pending
-
2024
- 2024-01-19 ZA ZA2024/00697A patent/ZA202400697B/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| US20230027740A1 (en) | 2023-01-26 |
| EP4373801A1 (en) | 2024-05-29 |
| KR20240027799A (en) | 2024-03-04 |
| ZA202400697B (en) | 2024-10-30 |
| EP4373801A4 (en) | 2025-12-10 |
| WO2023003898A1 (en) | 2023-01-26 |
| JP2024527846A (en) | 2024-07-26 |
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